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DK173556B1 - Polyol esters, their preparation and pharmaceutical use - Google Patents

Polyol esters, their preparation and pharmaceutical use Download PDF

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DK173556B1
DK173556B1 DK198404072A DK407284A DK173556B1 DK 173556 B1 DK173556 B1 DK 173556B1 DK 198404072 A DK198404072 A DK 198404072A DK 407284 A DK407284 A DK 407284A DK 173556 B1 DK173556 B1 DK 173556B1
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polyol
molecular weight
active agent
ester
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DK407284A (en
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Thomas Kissel
Zdenek Brich
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Novartis Ag
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/66Polyesters containing oxygen in the form of ether groups
    • C08G63/664Polyesters containing oxygen in the form of ether groups derived from hydroxy carboxylic acids
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/14Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles
    • A61K9/16Agglomerates; Granulates; Microbeadlets ; Microspheres; Pellets; Solid products obtained by spray drying, spray freeze drying, spray congealing,(multiple) emulsion solvent evaporation or extraction
    • A61K9/1605Excipients; Inactive ingredients
    • A61K9/1629Organic macromolecular compounds
    • A61K9/1641Organic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polyethylene glycol, poloxamers
    • A61K9/1647Polyesters, e.g. poly(lactide-co-glycolide)
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/20Pills, tablets, discs, rods
    • A61K9/2004Excipients; Inactive ingredients
    • A61K9/2022Organic macromolecular compounds
    • A61K9/2031Organic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polyethylene glycol, polyethylene oxide, poloxamers
    • A61K9/204Polyesters, e.g. poly(lactide-co-glycolide)
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/02Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
    • C08G63/06Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from hydroxycarboxylic acids
    • C08G63/08Lactones or lactides
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S977/00Nanotechnology
    • Y10S977/902Specified use of nanostructure
    • Y10S977/904Specified use of nanostructure for medical, immunological, body treatment, or diagnosis
    • Y10S977/915Therapeutic or pharmaceutical composition

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  • Health & Medical Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Pharmacology & Pharmacy (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Epidemiology (AREA)
  • Polymers & Plastics (AREA)
  • Animal Behavior & Ethology (AREA)
  • General Health & Medical Sciences (AREA)
  • Public Health (AREA)
  • Veterinary Medicine (AREA)
  • Medicinal Preparation (AREA)
  • Polyesters Or Polycarbonates (AREA)
  • Medicines That Contain Protein Lipid Enzymes And Other Medicines (AREA)

Description

DK 173556 B1DK 173556 B1

Den foreliggende opfindelse angår en hidtil ukendt ester af en polyol, der er ejendommelig ved det i krav 1's kendetegnende del angivne. Opfindelsen angår også et reaktionsprodukt som angivet i krav 2, idet udførelsesformer herfor er angivet i krav 3-5. Opfindelsen angår endvidere end fremgangsmåde til fremstilling af et produkt 5 ifølge krav 1, hvilken fremgangsmåde er ejendommelig ved det i krav 6’s kendetegnende del angivne. Opfindelsen angår desuden depotmatrixmaterialer som angivet i krav 7 og 8 samt et parenteralt farmaceutisk depotpræparat til anvendelse som implantat eller mikrokapsler som angivet i krav 9 og 10.The present invention relates to a novel ester of a polyol which is characterized by the characterizing part of claim 1. The invention also relates to a reaction product as claimed in claim 2, embodiments thereof being given in claims 3-5. The invention further relates to a method for producing a product 5 according to claim 1, which is characterized by the characterizing part of claim 6. The invention further relates to depot matrix materials as claimed in claims 7 and 8 and a parenteral pharmaceutical depot preparation for use as implant or microcapsules as claimed in claims 9 and 10.

10 En bred klasse af polyolestere med polymere hydroxycarboxyliske esterrester er beskrevet i DE patentskrift nr. 1.020.034, hvori glycerolestere med polylactidestererest af 30 mælkesyrerester eller pentaerythritolester med polymælkesyrerest af 16 mælkesyrerester specifikt er beskrevet. I patentskriftet er der ikke specifikt beskrevet længere kædepolymerestere af polyoler med mindst 3 hydroxygrupper.A broad class of polyol esters with polymeric hydroxycarboxylic ester residues is disclosed in DE patent specification 1,020,034, in which glycerol esters having polylactide ester residues of 30 lactic acid residues or pentaerythritol esters having polylactic acid residues of 16 lactic acid residues are specifically described. The patent does not specifically describe longer chain polymer esters of polyols having at least 3 hydroxy groups.

1515

Disse produkter anvendes som opløsningsmidler, fx til farmaceutiske formål, som emulgatorer eller som additiver til syntetiske materialer og plastmaterialer. Der er ingen beskrivelse af deres anvendelse til farmaceutiske depotmatrixpræparater.These products are used as solvents, for example, for pharmaceutical purposes, as emulsifiers or as additives for synthetic and plastic materials. There is no description of their use in pharmaceutical matrix compositions.

20 *20 *

Estere af sukkeralkoholer, fx ud fra erythritol, xylitol, ribitol og sorbitol, med poly-s-hydroxycapronsyre er beskrevet i Journal of Polymer Science, Polymer Chemistry Edition, 20, 1982, s. 319-326, især s. 323-326.Esters of sugar alcohols, for example, from erythritol, xylitol, ribitol and sorbitol, with poly-s-hydroxycaproic acid are described in Journal of Polymer Science, Polymer Chemistry Edition, 20, 1982, pp. 319-326, especially pp. 323-326.

25 Molekylvægten af disse estere afhænger af esterificeringsgraden af hydroxygrupperne i polyolesterne og af længden af poly-e-hydroxy-capronsyreresterne. Størrelsesordenen er fra ca. 26.000 til 65.000.The molecular weight of these esters depends on the degree of esterification of the hydroxy groups in the polyol esters and the length of the poly-e-hydroxy-capric acid residues. The order of magnitude is from approx. 26,000 to 65,000.

Esterne har stjernepolymerstruktur, idet deres enkelte polyolrest som 20 den centrale del er omgivet af syrerestkæder. Der er ikke nævnt nogen anvendelse af polyolesterne i dette litteratursted.The esters have star polymer structure, with their single polyol residue as the central portion being surrounded by acid residue chains. No use of the polyol esters in this literature site has been mentioned.

Diffusionshastigheden for farmakologisk aktive midler fra esteren og esterens nedbrydningshastighed som matrixmateriale for aktive midler er for ringe til praktisk anvendelse som implantat eller mikrokapsei.The rate of diffusion of pharmacologically active agents from the ester and the rate of degradation of the ester as matrix material for active agents are too poor for practical use as implant or microcapsia.

03 På grund af poly-s-hydroxycapronsyreresternes hydrofobe egenskaber er esterne ikke egnede som matrixmateriale til depotformer af farmakologisk aktive midler.03 Due to the hydrophobic properties of poly-s-hydroxycaproic acid residues, the esters are not suitable as matrix material for depot forms of pharmacologically active agents.

DK 173556 B1 2DK 173556 B1 2

Adskillige depotformer af farmakologisk aktive midler har været foreslået i litteraturen. I EP patentansøgning nr. 92.918 er beskrevet polypeptider i en matrix af en ester af fx polyvinylalkohol (molekylvægt 14.000) eller polyethylenglycol (molekylvægt 6000 eller 20.000) indeholdende polymere hydroxycarboxylesterrester, fx fra mælkesyre 5 (molekylvægt 26.000-114.000) og undertiden også glycolsyre (molekylvægt 10.000).Several forms of pharmacologically active agents have been proposed in the literature. EP Patent Application No. 92,918 discloses polypeptides in an ester matrix of, for example, polyvinyl alcohol (molecular weight 14,000) or polyethylene glycol (molecular weight 6,000 or 20,000) containing polymeric hydroxycarboxylic ester residues, e.g. from lactic acid 5 (molecular weight 26,000-114,000) and sometimes also glycol acid 10,000).

Matrixmaterialer med store molekylære andele af sådanne polyolradika-ler har imidlertid alt for hydrofile egenskaber og bliver for hurtigt nedbrudt under brugsbetingelser.However, matrix materials with large molecular proportions of such polyol radicals have far too hydrophilic properties and degrade too quickly under conditions of use.

1010

Disse matrixmaterialers stærke hydrofile egenskaber og blødhed besværliggør endvidere produktionen deraf, den yderligere forarbejdning og anvendelsen af depotformer, især mikrokapsler.Furthermore, the strong hydrophilic properties and softness of these matrix materials impede the production thereof, the further processing and use of deposit forms, especially microcapsules.

Som estere nævnes endvidere fx dextran som en polyol, men på grund 15 af dextraners høje molekylvægt er en sådan esterdannelse praktisk taget umulig.Furthermore, as esters, for example, dextran is mentioned as a polyol, but due to the high molecular weight of dextran such an ester formation is practically impossible.

Depotformer af farmakologisk aktive midler i en matrix af en polymer af polyoler og hydroxycarboxylsyrer er foreslået som del af en meget bred klasse af produkter i 20 international patentansøgning WO 78/00011. Imidlertid er der ikke givet eksempler på polymerer af polyoler og hydroxymonocarboxylsyrer. Der er angivet eksempler på depotformer af polyolestere ineholdende polymere dicarboxylsyrerester, fx af vinsyre.Deposits of pharmacologically active agents in a matrix of a polymer of polyols and hydroxycarboxylic acids are proposed as part of a very broad class of products in International Patent Application WO 78/00011. However, no examples of polymers of polyols and hydroxymonocarboxylic acids have been provided. Examples of depot forms of polyol esters containing polymeric dicarboxylic acid residues, e.g., of tartaric acid, are provided.

Disse polyolestere har en struktur, der adskiller sig fra de ovenfor 25 beskrevne produkter. De har en lineær kæde og indeholder alternativt polyol rester og dicarboxylsyrerester.These polyol esters have a structure different from the products described above. They have a linear chain and alternatively contain polyol residues and dicarboxylic acid residues.

De dannede estere har så lav en opløselighed, at der må dannes opløselige prækondensater for at inkorporere de farmakologisk aktive midler. Kun da kan det prækondenserede aktive middel indeholdende ou matrixmaterialer kondenseres yderligere.The esters formed have such a solubility that soluble precondensates must be formed to incorporate the pharmacologically active agents. Only then can the precondensed active agent containing ou matrix materials be further condensed.

35 DK 173556 B1 335 DK 173556 B1 3

Hvis der anvendes mættede dicarboxylsyrer, fx vinsyre, er det angivet, at den endelige totale kondensation skal udfores ved forhøjet temperatur (ca. 170-200°C), hvilket ikke er egnet til varmefølsomme aktive midler.If saturated dicarboxylic acids are used, eg tartaric acid, it is indicated that the final total condensation must be carried out at elevated temperature (about 170-200 ° C), which is not suitable for heat sensitive active agents.

55

Under anvendelse af pentaerythritol som polyol dannes stærkt tvær-bundne produkter, som ikke er egnede til inkorporering af farmakologisk aktive midler, og som ikke nedbrydes tilstrækkeligt hurtigt in vivo.Using pentaerythritol as polyol, highly crosslinked products are formed which are not suitable for incorporation of pharmacologically active agents and which do not degrade sufficiently rapidly in vivo.

1010

Massenedbrydningshastigheden for depotpræparater fremstillet ud fra disse materialer er for langsom.The mass decomposition rate of depot preparations made from these materials is too slow.

Den beskrevne fremstillingsproces til fremstilling af mikrokapslerne -|5 eller andre depotformer er ligeledes omstændelig.The manufacturing process described for the preparation of the microcapsules - 5 or other storage forms is similarly cumbersome.

De kendte matrixpolymerer har generelt en ufordelagtigt kort eller lang nedbrydningstid under brugsbetingelser, fx i legemet, i sammenligning med den nødvendige frigørelsestid for det farmakologisk aktive middel, hvilket fører til, at de aktive midler enten forsvinder for 20 , hurtigt sammen med matrixmaterialet eller forsvinder helt fra den endnu tilstedeværende polymermatrix. Der kan derfor ikke senere administreres en yderligere dosis af depotformen, da der så kan ske uønsket akkumulering af polymert matrixmateriafe.The known matrix polymers generally have a disadvantageously short or long degradation time under conditions of use, for example in the body, in comparison with the required release time of the pharmacologically active agent, which causes the active agents to either disappear by 20, rapidly together with the matrix material or disappear completely. from the polymer matrix still present. Therefore, no further dose of the depot form can be administered later, since undesirable accumulation of polymeric matrix material may occur.

25 Den foreliggende opfindelses formål er at overvinde de ovenfor anførte ulemper og tilvejebringe en nyttig farmaceutisk depotform til klinisk anvendelse.The object of the present invention is to overcome the above-mentioned drawbacks and to provide a useful pharmaceutical depot form for clinical use.

Depotformer, der er fremstillet ud fra polyofesterne ifølge den foreliggende opfindelse, 30 har endvidere den fordel, at de har en medikamentfrigørelsestid, som er tilfredsstillende lang, fx 1 måned, og derefter en kort nedbrydningsperiode for massen. De kan anvendes til inkorporering af en lang række fx vandopløselige eller hydrofobe aktive midler.Further, depot forms prepared from the polyofester of the present invention have the advantage of having a drug release time which is satisfactorily long, e.g., 1 month, and then a short degradation period for the pulp. They can be used to incorporate a wide variety of e.g. water-soluble or hydrophobic active agents.

35 4 DK 173556 B135 4 DK 173556 B1

Polyolesterne ifølge den foreliggende opfindelse kan derudover let håndteres og let oparbejdes til inkorporering af de aktive midler og til fremstilling af farmaceutiske præparatformer, fx mikrokapsler og implantater. Disse mikrokapsler er ikke bløde; de er derfor lette at 5 administrere gennem en injektionsnål.In addition, the polyol esters of the present invention can be easily handled and readily processed for incorporation of the active agents and for the preparation of pharmaceutical formulations, e.g., microcapsules and implants. These microcapsules are not soft; they are therefore easy to administer through an injection needle.

Den foreliggende opfindelse angår en ester af en polyol, hvilken polyol indeholder mindst 3 hydroxygrupper og har en molekylvægt på op til 20.000, hvorhos mindst én hydroxygruppe i polyolen er i form 10 af en ester, med en poly- eller co-polymælkesyrerest, som hver har en molekylvægt på mindst 5000, fx fra 5000 til fx 85.000. Et andet aspekt af den foreliggende opfindelse angår et reaktionsprodukt af en polyol indeholdende mindst 3 hydroxygrupper og med en molekylvægt på op til 20.000 eller et reaktivt derivat deraf og mælkesyre eller et reaktivt 15 derivat og, om ønsket, mindst én yderligere hydroxycarboxylsyre eller et funktionelt derivat deraf, hvilket produkt har en polymerkæde med en molekylvægt på mindst 5000. Disse produkter betegnes "poly-olestere ifølge opfindelsen".The present invention relates to an ester of a polyol, said polyol containing at least 3 hydroxy groups and having a molecular weight of up to 20,000, wherein at least one hydroxy group in the polyol is in the form of an ester, with a poly or co-poly lactic acid residue, each of which has a molecular weight of at least 5000, for example from 5000 to, for example, 85,000. Another aspect of the present invention relates to a reaction product of a polyol containing at least 3 hydroxy groups and having a molecular weight of up to 20,000 or a reactive derivative thereof and lactic acid or a reactive derivative and, if desired, at least one additional hydroxycarboxylic acid or functional derivative thereof, having a polymer chain having a molecular weight of at least 5000. These products are referred to as "polyol esters of the invention".

20 P°lyolresterne er især af en polyol indeholdende en kæde af carbon -atomer. En særlig polyolform er en sådan, som har lineær struktur og indeholder 3-6, især 6, hydroxygrupper. Egnede polyoler med lineær struktur omfatter fx mannitol, pentaerythritol, sorbitol, ribito! og xylitol. Andre foretrukne polyolformer er former med cyclisk struktur og indeholdende 4-30 hydroxygrupper.In particular, the 20 P lyol residues are of a polyol containing a chain of carbon atoms. A particular polyol form is one which has linear structure and contains 3-6, especially 6, hydroxy groups. Suitable linear structure polyols include, for example, mannitol, pentaerythritol, sorbitol, ribito! and xylitol. Other preferred polyol forms are cyclic structure forms containing 4-30 hydroxy groups.

2525

Polyolerne med cyclisk struktur indeholder især én eller flere saccha-ridenheder og har mindst 3 hydroxygrupper pr. enhed. Eksempler på sådanne polyoler er polyoler med fructosestruktur, fx fructose selv.In particular, the cyclic structure polyols contain one or more saccharide units and have at least 3 hydroxy groups per unit. Examples of such polyols are polyols with fructose structure, for example fructose itself.

Særlige polyoler med cyclisk struktur er sådanne, som har glucose-30 struktur, fx glucose selv, eller som har 2-8 glucoseenheder. Disse enheder er fortrinsvis forbundet i 1,4- og/elier 1,6-stilling, især i 1.4- stilling. En polyol indeholdende flere glucoseenheder forbundet i 1.4- stilling er fx f5-cyclodextrin.Particular cyclic structure polyols are those which have glucose structure, e.g., glucose itself, or which have 2-8 glucose units. These units are preferably connected in the 1.4 and / or 1.6 positions, especially in the 1.4 position. A polyol containing several glucose units linked in the 1.4 position is, for example, f5-cyclodextrin.

35 5 DK 173556 B135 5 DK 173556 B1

Den foretrukne polyol er glucose.The preferred polyol is glucose.

Polyolesterne kan have fx en polyolrest med mindst 3 hydroxygrupper i form af estere, som indeholder polylactid- eller co-poiylactidkæder. Deres struktur kan være således 5 forgrenet, dvs. være stjerneformet. Enhver sådan kæde har fortrinsvis identiske hydroxycarboxylsyrerester.The polyol esters may have, for example, a polyol residue having at least 3 hydroxy groups in the form of esters containing polylactide or copolylactide chains. Thus, their structure may be branched, i.e. be star-shaped. Preferably, any such chain has identical hydroxycarboxylic acid residues.

Kæderne kan indeholde lactidrester alene. De kan alternativt indeholde yderligere fx 1, 2, 3 eller flere specifikke hydroxycarboxylsyre-10 rester, fx op til 70 molprocent, fx 30-70 molprocent.The chains may contain lactide residues alone. Alternatively, they may contain further, for example, 1, 2, 3 or more specific hydroxycarboxylic acid residues, for example up to 70 mole percent, for example 30-70 mole percent.

Foretrukne ekstrarester er glycolsyrerester. Der forekommer fortrinsvis op til 70 molprocent, fx 30-70 molprocent, især 50 molprocent, glycolsyreenheder. I stedet for eller ud over glycolsyreenhederne kan der forekomme andre forskellige enheder, fx ε-hydroxycapronsyreen-15 heder, fortrinsvis op til 20 molprocent.Preferred auxiliary residues are glycolic acid residues. Preferably, up to 70 mole percent, e.g., 30-70 mole percent, especially 50 mole percent, of glycolic acid units are present. Instead of or in addition to the glycolic acid moieties, there may be other various moieties, e.g., ε-hydroxycaproic acids, preferably up to 20 mole percent.

Mælkesyreenhederne kan forekomme i optisk ren form (D- eller L-lac-tidform) eller som blanding deraf, fx deres racemiske form (D,L-lac-tidform).The lactic acid units may occur in optically pure form (D or L-lac time form) or as a mixture thereof, e.g., their racemic form (D, L-lac time form).

2020

Den foreliggende opfindelse angår endvidere en fremgangsmåde til fremstilling af et produkt ifølge opfindelsen, hvilken fremgangsmåde er ejendommelig ved, at en polyol med en molekylvægt på op til 20.000 og med mindst 3 hydroxygrupper eller et reaktivt derivat deraf 25 esterificeres med mælkesyre eller et reaktivt derivat deraf og, om ønsket, med mindst én yderligere hydroxycarboxylsyre eller et funktionelt derivat deraf.The present invention further relates to a process for the preparation of a product according to the invention, characterized in that a polyol having a molecular weight of up to 20,000 and having at least 3 hydroxy groups or a reactive derivative thereof is esterified with lactic acid or a reactive derivative thereof. and, if desired, with at least one additional hydroxycarboxylic acid or a functional derivative thereof.

Fremgangsmåden er især ejendommelig ved, at en polyol med en molekylvægt på op til 20.000 og med mindst 3 hydroxygrupper omsættes 30 med mælkesyre eller desuden med mindst én yderligere hydroxycarboxylsyre i lacton- eller dimer cyclisk esterform i nærværelse af en katalysator, som muliggør ringåbningspolymerisation.The process is particularly characterized in that a polyol having a molecular weight of up to 20,000 and having at least 3 hydroxy groups is reacted with lactic acid or in addition with at least one additional hydroxycarboxylic acid in lactone or dimer cyclic ester form in the presence of a catalyst which allows ring-opening polymerization.

6 DK 173556 B16 DK 173556 B1

Katalysatoren er fortrinsvis Sn-octoat.The catalyst is preferably Sn-octoate.

Reaktionskomponenterne blandes fx med katalysatoren og omsættes ved forhøjet temperatur.For example, the reaction components are mixed with the catalyst and reacted at elevated temperature.

Hvis der forekommer et opløsningsmiddel, fx toluen, kan komponenter-5 ne omsættes ved opløsningsmidlets tilbagesvalingstemperatur. Uden opløsningsmiddel kan reaktionstemperaturen være højere, hvis der fx som polyol anvendes glucose, op til ca. 170°C, og hvis der anvendes β-cyclodextrin, op til 180°C. Reaktionen foretages fortrinsvis i fravær af vand.If a solvent, e.g. toluene, is present, the components may be reacted at the reflux temperature of the solvent. Without solvent, the reaction temperature can be higher if, for example, as polyol glucose is used, up to approx. 170 ° C and if β-cyclodextrin is used, up to 180 ° C. The reaction is preferably carried out in the absence of water.

10 Den dannede polyolester ifølge opfindelsen kan renses og isoleres på sædvanlig måde.The polyol ester formed according to the invention can be purified and isolated in the usual manner.

Bestemmelsen af molekylvægten af det rensede produkt kan foretages under anvendelse af sædvanlige metoder, fortrinsvis ved gelpermeati-onschromatografi (GPC) under anvendelse af polystyren som standard 15 (Mw), Dupont Ultrastyragel® 500 Å og 10.0000 Λ som søjle og tetra- hydrofuran som opløsningsmiddel, ved stuetemperatur.The molecular weight of the purified product can be determined using conventional methods, preferably by gel permeation chromatography (GPC) using polystyrene as standard 15 (Mw), Dupont Ultrastyragel® 500 Å and 10,0000 Λ as column and tetrahydrofuran as solvent. , at room temperature.

Molekylvægten (Mw) af polyolesterne ifølge opfindelsen ligger fortrinsvis på mellem 20.000 og 200.000, fx på mellem 20.000 og 80.000.The molecular weight (Mw) of the polyol esters of the invention is preferably between 20,000 and 200,000, for example between 20,000 and 80,000.

Molekylvægten af polyolesterne ifølge opfindelsen afhænger af vægtfor-20 holdet mellem komponenterne i reaktionen og af reaktionsbetingelserne, fx reaktionstemperaturen (jfr. eksempel 8). Lavere reaktionstemperatur kan føre til kortere polymerkæder og således til polyolestere med lavere molekylvægt.The molecular weight of the polyol esters of the invention depends on the weight ratio of the components of the reaction and the reaction conditions, e.g., the reaction temperature (cf. Example 8). Lower reaction temperature can lead to shorter polymer chains and thus to lower molecular weight polyol esters.

Isoleringen og rensningen kan påvirke molekylvægten af den rensede 25 polyolester. Ændring af isolerings- og rensningsbetingelserne fører til en ændring af molekylvægten (jfr. eksempel 2). Da polyolesteren generelt i praksis kan forekomme som en blanding af molekyler med kæder af forskellig længde, kan denne blandings sammensætning påvirkes af isolerings- og rensningsmetoder, fx ekstraktion, filtrering 30 og isolerings- og rensningsvæskerne og mængden deraf og isolerings-og rensningstemperaturen.The insulation and purification may affect the molecular weight of the purified polyol ester. Changing the isolation and purification conditions leads to a change in molecular weight (cf. example 2). In general, since the polyol ester may appear as a mixture of molecules of different length chains, the composition of this mixture may be influenced by insulation and purification methods, for example, extraction, filtration and the isolation and purification fluids, and the amount thereof and the isolation and purification temperature.

7 DK 173556 B17 DK 173556 B1

Molekylvægten af den rensede polymer kan forøges ved at fjerne forbindelser med lav molekylvægt, fx ved egnet udfældning af polymeren, fx i methanol, eller ved membranfiltrering.The molecular weight of the purified polymer can be increased by removing low molecular weight compounds, for example, by suitable precipitation of the polymer, for example in methanol, or by membrane filtration.

Mængden af komponenter med lav molekylvægt kan reduceres ved 5 membranfiltrering i en sådan grad, at deres toppe i molekylvægtspektret bestemt ved GPC tilsammen har en højde på op til 10%, fortrinsvis op til 7%, af højden af polymerens Mw-top.The amount of low molecular weight components can be reduced by membrane filtration to such an extent that their peaks in the molecular weight spectrum determined by GPC together have a height of up to 10%, preferably up to 7%, of the height of the polymer's Mw peak.

Opfindelsen angår således også et produkt, i hvilket de individuelle toppe for lav molekylvægt ifølge GPC tilsammen udgør op til 10% af 10 højden af polyesterens Mw-top.The invention thus also relates to a product in which the individual low molecular weight peaks according to GPC together constitute up to 10% of the height of the polyester Mw peak.

Polyolesterne ifølge opfindelsen er særlig velegnede til inkorporering af aktive midler og giver forlænget frigørelseseffekt af de aktive midler i kroppen.The polyol esters of the invention are particularly well suited for incorporating active agents and provide prolonged release effect of the active agents in the body.

Balancen mellem hydrofobe og hydrofile faktorer - polyolresten repræ-15 senterer den hydrofile faktor og polylactid- eller co-polylactidresten den hydrofobe faktor - kan reguleres ved at ændre polyolerne, hydr-oxygruppernes esterificeringsgrad, de polymere kæders længde og identitet og de relative mængder af de pågældende hydroxycarboxyl-syreenheder i kæden.The balance between hydrophobic and hydrophilic factors - the polyol residue represents the hydrophilic factor and the polylactide or co-polylactide residue the hydrophobic factor - can be regulated by changing the polyols, the degree of esterification of the hydroxy groups, the length and identity of the polymer chains, and the relative amounts of the hydroxycarboxylic acid units in the chain.

20 Polyolesterne ifølge opfindelsen er derfor særlig velegnede til fremstilling af farmaceutiske depotpræparater indeholdende farmakologisk aktive midler. Sådanne depotpræparater kan forekomme som en polyol-estermatrix indeholdende det aktive middel. Foretrukne depotformer er implantater (fx til subcutan administration) og mikrokapsler (fx til 25 oral eller især til parenteral, fx intramuskulær, administration).The polyol esters of the invention are therefore particularly suitable for the preparation of pharmaceutical depot preparations containing pharmacologically active agents. Such depot preparations may appear as a polyol ester matrix containing the active agent. Preferred depot forms are implants (e.g., for subcutaneous administration) and microcapsules (e.g., for oral or especially for parenteral, e.g., intramuscular, administration).

Opfindelsen angår derfor også en farmaceutisk depotform med en matrix af esteren ifølge opfindelsen og indeholdende et farmakologisk aktivt middel.The invention therefore also relates to a pharmaceutical depot form having a matrix of the ester of the invention and containing a pharmacologically active agent.

Depotformerne er hidtil ukendte og udgør et aspekt af den forelig-30 gende opfindelse.The deposit forms are novel and constitute an aspect of the present invention.

8 DK 173556 B18 DK 173556 B1

Depotformerne kan fremstilles pi sædvanlig måde, idet polyolesterne ifølge opfindelsen let håndteres, og idet der ofte inkorporeres en høj koncentration af det aktive middel.The depot forms can be prepared in the usual manner, the polyol esters of the invention being readily handled and often having a high concentration of the active agent incorporated.

Til fremstilling af mikrokapsler kan det aktive middel opløses i et 5 flygtigt opløsningsmiddel, fx methylenchlorid. En opløsning af polyol-esteren, fx i samme opløsningsmiddel, kan derefter tilsættes, og den resulterende blanding kan sprøjtes ind i luft, medens temperaturen reguleres omhyggeligt, og derefter tørres til dannelse af mikrokapsler.For the preparation of microcapsules, the active agent can be dissolved in a volatile solvent, for example methylene chloride. A solution of the polyol ester, for example in the same solvent, can then be added and the resulting mixture can be injected into air while the temperature is carefully controlled and then dried to form microcapsules.

10 Alternativt kan det aktive middel opløses eller suspenderes, fx i methylendichlorid, og polyolesteren kan opløses i et flygtigt, med vand ikke-blandbart opløsningsmiddel, fx methylendichlorid, hvorefter den organiske fase kan blandes grundigt med en omrørt vandig opløsning, fx pufret til pH 7, og eventuelt indeholdende fx gelatine som 15 emulgator. Det organiske opløsningsmiddel kan derefter fjernes fra den resulterende emulsion, og de resulterende mikrokapsler kan frafiltreres eller fraskilles ved centrifugering, vaskes, fx i en puffer, og tørres.Alternatively, the active agent may be dissolved or suspended, e.g., in methylene dichloride, and the polyol ester may be dissolved in a volatile, water-immiscible solvent, e.g., methylene dichloride, after which the organic phase may be thoroughly mixed with a stirred aqueous solution, e.g., buffered to pH 7 , and optionally containing, for example, gelatin as an emulsifier. The organic solvent can then be removed from the resulting emulsion and the resulting microcapsules filtered off or separated by centrifugation, washed, for example, in a buffer, and dried.

Til fremstilling af implantater kan det aktive middel blandes med 20 polyolesteren og opløses i et flygtigt opløsningsmiddel, opløsningsmidlet kan afdampes og remanensen formales. Der kan dannes et ekstru-sionspræparat på sædvanlig måde, som derefter presses, fx til implantattabletter på 5-15, især 7 mm, og med 20-80 mg, fx 20-25 mg, matrixmateriale ved 75°C og 80 bar i 10-20 minutter.For preparing implants, the active agent can be mixed with the polyol ester and dissolved in a volatile solvent, the solvent can be evaporated and the residue ground. An extrusion preparation may be formed in the usual manner, which is then pressed, for example into implant tablets of 5-15, especially 7 mm, and with 20-80 mg, e.g. 20-25 mg, matrix material at 75 ° C and 80 bar for 10 minutes. -20 minutes.

25 Alt afhængig af det aktive middel kan mikrokapslerne optage gennemsnitlig op til 60 vægtprocent af det aktive middel. Implantaterne fremstilles fortrinsvis på en sådan måde, at de indeholder op til 60, fx 1-20, vægtprocent af det aktive stof.25 Depending on the active agent, the microcapsules can absorb on average up to 60% by weight of the active agent. The implants are preferably manufactured in such a way that they contain up to 60, e.g., 1-20, weight percent of the active substance.

Til det aktive middel bromocryptin kan der fremstilles mikrokapsler 30 indeholdende højst 25 vægtprocent, især op til 18 vægtprocent, og implantater indeholdende op til 18 vægtprocent, af det aktive middel.For the active agent bromocryptin, microcapsules 30 containing up to 25% by weight, especially up to 18% by weight, and implants containing up to 18% by weight, of the active agent may be prepared.

9 DK 173556 B19 DK 173556 B1

Mikrokapslerne kan have en diameter på fra nogle submikron til nogle millimeter. Til farmaceutiske mikrokapsler tilstræbes en diameter på højst ca. 250 mikron, fx 10-60 mikron, for at lette passagen gennem en injektionsnål.The microcapsules can have a diameter of from some submicron to a few millimeters. For pharmaceutical microcapsules, a diameter of no more than approx. 250 microns, eg 10-60 microns, to facilitate passage through an injection needle.

5 Depotpræparatet ifølge den foreliggende opfindelse kan anvendes til administration af en lang række klasser af aktive midler, fx farmakologisk aktive midler såsom kontraceptiva, sedativa, steroider, sulfonamider, vacciner, vitaminer, antimigrænemedikamenter, enzymer, bronchodilatatorer, cardiovasculære medikamenter, analgetika, antibio-10 tika, antigener, antikonvulsionsmedikamenter, antiinflammatoriske medikamenter, anti-Parkinson-medikamenter, prolactinsekretionsinhibitorer, antiastmamedikamenter, geriatika og antimalariamidler.The depot preparation of the present invention can be used to administer a wide variety of classes of active agents, e.g., pharmacologically active agents such as contraceptives, sedatives, steroids, sulfonamides, vaccines, vitamins, antimigraine drugs, enzymes, bronchodilators, cardiovascular drugs, analgesics, antibiotics. tika, antigens, anticonvulsant drugs, anti-inflammatory drugs, anti-Parkinson's drugs, prolactin secretion inhibitors, antiastema drugs, geriatrics and antimalarials.

Depotpræparaterne kan anvendes til de kendte indikationer for det pågældende inkorporerede aktive middel.The depot preparations may be used for the known indications of the incorporated active agent concerned.

15 De eksakte mængder aktivt middel og depotpræparat, der skal administreres, afhænger af et antal faktorer, fx den lidelse, der skal behandles, den ønskede behandlingsvarighed, det aktive middels frigø-reiseshastighed og polymermatrixens nedbrydelighed.The exact amounts of active agent and depot preparation to be administered depend on a number of factors, for example, the disorder to be treated, the desired duration of treatment, the rate of release of the active agent and the degradability of the polymer matrix.

De ønskede præparater kan fremstilles på kendt måde. Den mængde 20 farmakologisk aktivt middel, der er nødvendig, og dettes frigørelseshastighed kan fastlægges på basis af kendte in vitro- eller in vivo-teknikker, der fx er beskrevet i eksempel 26-29, fx hvor længe koncentrationen i blodplasma af et bestemt aktivt middel forbliver på et acceptabelt niveau. Matrixens nedbrydelighed kan også bestemmes 25 ved in vitro- eller især in vivo-teknikker, fx hvor mængden af matrix-materialer i en muskel vejes efter bestemte tidsrum.The desired compositions may be prepared in known manner. The amount of pharmacologically active agent needed and its rate of release may be determined on the basis of known in vitro or in vivo techniques described, for example, in Examples 26-29, e.g., how long the blood plasma concentration of a particular active agent is remains at an acceptable level. The degradability of the matrix can also be determined by in vitro or especially in vivo techniques, for example where the amount of matrix materials in a muscle is weighed after certain periods of time.

Depotpræparaterne ifølge opfindelsen kan administreres i form af fx mikrokapsler, fx oralt, fortrinsvis subcutant eller intramuskulært, fortrinsvis i form af eller i en suspension i et egnet flydende bære-30 stof eller i form af implantater, fx subcutant.The depot compositions of the invention may be administered in the form of, for example, microcapsules, for example, orally, preferably subcutaneously or intramuscularly, preferably in the form of or in a suspension in a suitable liquid carrier or in the form of implants, for example, subcutaneously.

10 DK 173556 B110 DK 173556 B1

Gentagen administration af depotpræparaterne ifølge opfindelsen kan foretages, når polyolestermatrixen er blevet tilstrækkeligt nedbrudt, fx efter 1 måneds forløb.Repeated administration of the depot compositions of the invention can be made when the polyol ester matrix has been sufficiently degraded, for example, after 1 month.

Eksempler på doser af foretrukne forbindelser er: 5 Til prolactinsekretionsinhibering med bromocryptin kan der fx fremstilles et intramuskulært depotpræparat, som daglig frigør 2,5-7,5 mg bromocryptin i ca. 30 dage og fx indeholder 70-230 mg bromocryp-tin-mesyfat.Examples of doses of preferred compounds are: 5 For prolactin secretion inhibition with bromocryptin, for example, an intramuscular depot preparation may be prepared which releases 2.5-7.5 mg of bromocryptin daily for approx. 30 days and, for example, contain 70-230 mg of bromocryp tin-mesyphate.

Til behandling af bronchial astma med ketotifen kan der fx fremstilles 10 et intramuskulært depotpræparat, som daglig frigør 0,5-0,8 mg ketotifen i ca. 30 dage og fx indeholder 15-25 mg ketotifen.For example, for the treatment of bronchial asthma with ketotifen, an intramuscular depot preparation may be prepared which releases 0.5-0.8 mg of ketotifen daily for approx. 30 days and for example contains 15-25 mg of ketotifen.

Til reaktivering af cerebral metabolisme med codergocrin kan der fx fremstilles et intramuskulært depotpræparat, som daglig frigør 0,1-0,4 mg codergocrin i ca. 30 dage og indeholder ca. 3-12 mg.For example, to reactivate cerebral metabolism with codergocrine, an intramuscular depot preparation may be prepared which releases 0.1-0.4 mg of codergocrine daily for approx. 30 days and contains approx. 3-12 mg.

15 Depotpræparater til andre aktive midler kan formuleres på analog måde, fx til at tilvejebringe den kendte passende, fx terapeutiske, koncentration af aktivt middel til parenteral anvendelse i et forlænget tidsrum, fx 30 dage.Deposits for other active agents may be formulated in an analogous manner, e.g., to provide the known appropriate, e.g., therapeutic, concentration of active agent for parenteral use for a prolonged period of time, e.g., 30 days.

Som anført ovenfor kan polymernedbrydningen følges i forsøg in vivo 20 og in vitro som beskrevet i eksempel 24 og 25. Det fremgår deraf, at polyolesterne ifølge opfindelsen nedbrydes hurtigere end tilsvarende kendte polylactid- og polylactid/glycolidsyrer, og der kan især iagttages en hurtigere nedbrydning i det tidlige stadium, fx op til 30 dage, især i tilfælde af polylactid/glycolid-polymerkæder.As noted above, polymer degradation can be monitored in experiments in vivo 20 and in vitro as described in Examples 24 and 25. It can be seen that the polyol esters of the invention degrade more rapidly than corresponding known polylactide and polylactide / glycolide acids, and more particularly degradation can be observed. in the early stage, for example up to 30 days, especially in the case of polylactide / glycolide polymer chains.

25 Membranfiltrering resulterer i residualpolymerprodukter, som generelt i det tidlige stadium, især op til 30 dage, har mindre massenedbrydningshastighed end hastigheden for det tilsvarende ufiltrerede produkt. I tilfælde af residualpolyolestere ifølge opfindelsen kan nedbrydningen være over 50% i op til 30 dage, og i det tilfælde, som er 30 beskrevet i eksempel 6, ca. 70%. Efter 40-50 dage kan nedbrydningen være praktisk taget fuldstændig.Membrane filtration results in residual polymer products, which generally have at the early stage, especially up to 30 days, less mass degradation rate than the rate of the corresponding unfiltered product. In the case of residual polyol esters of the invention, the degradation can be above 50% for up to 30 days, and in the case described in Example 6, approx. 70%. After 40-50 days the degradation can be practically complete.

11 DK 173556 B1 i frigørelseshastighedstests in vitro og in vivo kan polyolesterne ifølge opfindelsen frigøre det aktive middel med en hastighed, der er af samme orden som den, der er kendt hos tilsvarende kendte polymere poly- eller copolylactider, fx i løbet af 30 dage.In release rate tests in vitro and in vivo, the polyol esters of the invention can release the active agent at a rate which is of the same order as that of similar known polymeric poly or copolylactides, for example over 30 days.

55

De aktive midler kan hovedsagelig frigøres ved diffusion fra matrixen og kun i lille udstrækning ved nedbrydning af matrixmaterialet.The active agents can be released mainly by diffusion from the matrix and only to a small extent by degradation of the matrix material.

Dette resulterer i en mere regelmæssig frigørelseshastighed for det aktive middel.This results in a more regular release rate for the active agent.

1010

En fordel ved polyestermatrixerne ifølge opfindelsen er, at de efter praktisk taget fuldstændig frigørelse af aktivt middel hurtigt kan nedbrydes til en acceptabel størrelse, som af legemsvæskerne kan transporteres væk fra administrationsstedet.An advantage of the polyester matrices of the invention is that, after practically complete release of active agent, they can rapidly degrade to an acceptable size which can be transported away from the site of administration by the body fluids.

1515

Ifølge den foreliggende opfindelse er der tilvejebragt et parenteralt farmaceutisk depotpræparat til anvendelse som implantat eller mikro-kapsler indeholdende et farmakologisk aktivt middel indlejret eller indkapslet i en polymermatrix af en ester af en polyol ifølge krav 1, hvilket præparat er 20 tildannet til at frigøre alt eller i det væsentlige alt aktivt middel ] et forlænget tidsrum, og polymeren er tildannet således, at den nedbrydes tilstrækkeligt hurtigt til at blive transporteret væk fra administrationsstedet inden for 20 dage efter frigørelse af alt eller i det væsentlige alt det aktive middel.According to the present invention there is provided a parenteral pharmaceutical depot composition for use as implant or microcapsules containing a pharmacologically active agent embedded or encapsulated in a polymer matrix of an ester of a polyol according to claim 1, which composition is formed to release all or substantially all active agent] for a prolonged period of time and the polymer is formed such that it degrades sufficiently rapidly to be transported away from the site of administration within 20 days of release of all or substantially all of the active agent.

25 Opfindelsen belyses nærmere i nedenstående eksempler, i hvilke alle temperaturangivelser er ukorrigerede. HYFIO® er et kendt filterhjælpemiddel .The invention is further illustrated in the examples below, in which all temperature indications are uncorrected. HYFIO® is a known filter aid.

12 DK 173556 B112 DK 173556 B1

Polyolester ud fra D( + )-glucose, DL-dilactid og digfycolid EKSEMPEL 1 79,4 g (0,684 mol) diglycolid, 120,6 g (0,838 mol) DL-dilactid og 0,4 g (2,2 miHimol) D( + )-glucose (0,2%) anbringes i en 1,5 liters 5 kolbe og opvarmes til 135°C under omrøring i argonatmosfære, hvorefter 1 ml Sn-octoat tilsættes.Polyolester from D (+) -glucose, DL-dilactide and digfycolide Example 1 79.4 g (0.684 mol) diglycolide, 120.6 g (0.838 mol) DL-dilactide and 0.4 g (2.2 mlHimol) D (+) -glucose (0.2%) is placed in a 1.5 liter flask and heated to 135 ° C with stirring in argon atmosphere, after which 1 ml of Sn-octoate is added.

Reaktionen er exoterm. Temperaturen stiger ti! 172°C. Efter 5 minutter standses omrøringen, og den brune viskose blanding videreomsæt-tes ved 130-140°C i 17 timer. Efter afkøling tilsættes 500 ml methylen-10 dichlorid. Blandingen opløses i videst mulig udstrækning ved kogning, og opløsningsmidlet fraskilles. Denne fremgangsmåde gentages, hvorefter remanensen yderligere ekstraheres med 500 ml methylendi-chlorid. De samlede mørkebrune opløsninger (i alt 1500 ml) renses med 50 g HYFLO®, koncentreres til 500 ml og behandles med 500 mi 15 10%'s vandig HCI-opløsning til fjernelse af katalysatoren. Opløsningen vaskes fem gange med 500 ml vand til pH 4,5 og fortyndes til 1 liter med methylendichlorid.The reaction is exothermic. The temperature rises ten! 172 ° C. After 5 minutes, stirring is stopped and the brown viscous mixture is continued at 130-140 ° C for 17 hours. After cooling, add 500 ml of methylene dichloride. The mixture is dissolved as much as possible by boiling and the solvent is separated. This procedure is repeated and the residue is further extracted with 500 ml of methylene dichloride. The combined dark brown solutions (a total of 1500 ml) are purified with 50 g of HYFLO®, concentrated to 500 ml and treated with 500 ml of 10% aqueous HCl solution to remove the catalyst. The solution is washed five times with 500 ml of water to pH 4.5 and diluted to 1 liter with methylene dichloride.

Opløsningen behandles med MgSO^ og med HYFLO®, koncentreres til 500 ml og dryppes i løbet af 1/2 time til 3 liter methanol ved -60°C.The solution is treated with MgSO4 and with HYFLO®, concentrated to 500 ml and dipped over 3 hours to 3 liters of methanol at -60 ° C.

20 Ved denne temperatur omrøres blandingen i 3 timer. Derefter frafiltre-res produktet og tørres ved 40°C i vakuum.At this temperature, the mixture is stirred for 3 hours. The product is then filtered off and dried at 40 ° C in vacuo.

Molekylvægten bestemmes ved gelpermeationschromatografi (GPC):The molecular weight is determined by gel permeation chromatography (GPC):

Mw = 34.800, Mn = 19.600, Mw/Mn = 1,77.Mw = 34,800, Mn = 19,600, Mw / Mn = 1.77.

Syretal: 6,8.Acid number: 6.8.

25 Ikke-omsat lactid: 1,7%.25 Unreacted lactide: 1.7%.

Ikke-omsat glycolid: <0,4%.Unreacted glycolide: <0.4%.

Molforhold glycolid/lactid i polymerkæderne: 45/55.Mole ratio glycolide / lactide in the polymer chains: 45/55.

NMR-Spektrum (CDCI^), 360 MHz: 5,20 (m, 0,55H, -CH-mælkesyre), 4,82 (m, 0,9H, -CH2-g!ycolsyre) og 1,58 (m, 3H, -CH^-mælkesyre).NMR Spectrum (CDCl3), 360 MHz: 5.20 (m, 0.55H, -CH-lactic acid), 4.82 (m, 0.9H, -CH2-glycolic acid) and 1.58 (m , 3H, -CH2-lactic acid).

13 DK 173556 B1 IR-Spektrum (CH,CU: v = 2950 (w, CH~); 1760 (s, -COOR);IR spectrum (CH, CU: v = 2950 (w, CH ~); 1760 (s, -COOR);

Jm £ ΓΠ3 X JJm £ ΓΠ3 X J

1390 og 1420 (w, CH^); 1160 (s, -O-) og 1090 (s, -0-) cm \ EKSEMPEL 2-51390 and 1420 (w, CH 2); 1160 (s, -O-) and 1090 (s, -0-) cm \ EXAMPLES 2-5

Analogt med det i eksempel 1 beskrevne fremstilles nedenstående 5 polyestere:By analogy with the example described in Example 1, the following 5 polyesters are prepared:

Eks. 2* 3* 45Ex. 2 * 3 * 45

Polyol 4 mg C^- 3,85 mg D( + )- 0,2 g D( + )- 0,2 g D( + )- 10 D(+)-glucose glucose + 0,15 glucose glucose (0,2%) mg D( + )-1C14- (0,2%) (0,2%) glucose DL-Di- 1,2 g 1,2 g 60,3 g 60,3 g 15 lactidPolyol 4 mg C ^ - 3.85 mg D (+) - 0.2 g D (+) - 0.2 g D (+) - 10 D (+) - glucose glucose + 0.15 glucose glucose (0, 2%) mg D (+) -1C14- (0.2%) (0.2%) glucose DL-Di-1.2 g 1.2 g 60.3 g 60.3 g lactide

Diglycolid 0,8 g 0,8 g 39,7 g 39,7 gDiglycolide 0.8 g 0.8 g 39.7 g 39.7 g

Sn-Octoat 10 vi 10 yl 0,5 ml 0,5 ml 20 _Sn-Octoat 10 vi 10 µl 0.5 ml 0.5 ml 20

Reak.- - - 168° C 155°CReaction - - - 168 ° C 155 ° C

temp.temp.

Mw 31.400 26.400 34.600 23.600 25 _VAT 31,400 26,400 34,600 23,600 25 _

Mn 17.300 10.600 20.700 13.300 14 DK 173556 B1Mn 17,300 10,600 20,700 13,300 14 DK 173556 B1

Eks. 2* 3* 45Ex. 2 * 3 * 45

Mw/Mn 1,81 2,50 1,67 1,77 5___Mw / Mn 1.81 2.50 1.67 1.77 5___

Molforhoid lactid/glycolid - - 55/45 58/42Molphoroid lactide / glycolide - - 55/45 58/42

Syretal - - 5,7 8,0 10___ I kke-omsat lactid og - - 0,6% <0,4% glycol id - - <0,4% <0,2% 15 * Vedrørende analyseresultater, jfr. nedenfor.Acid number - - 5.7 8.0 10___ In non-reacted lactide and - - 0.6% <0.4% glycol id - - <0.4% <0.2% 15 * For analysis results, cf. below.

Ad eksempel 2:Example 2:

Stoffet blev fremstillet for ved analyse at vise, at glucosen blev inkorporeret i polymeren, og at der virkelig blev dannet en polyol-ester.The substance was prepared to show by analysis that the glucose was incorporated into the polymer and that a polyol ester was really formed.

20 Der blev optaget målinger for intensivere NMR-signalet for glucosen.Measurements were taken to intensify the NMR signal for the glucose.

13 1313 13

Glucosen var en ren C -mærket glucose med 98,3 atomprocent CThe glucose was a pure C-labeled glucose with 98.3 atomic percent C

(LOT nr. 2358-4 MSD ISOTOPES, Merck, Canada).(LOT No. 2358-4 MSD ISOTOPES, Merck, Canada).

13 NMR-Signalet for C -glucoseudgangsmaterialet blev sammenlignet med 13 signalet for C -giucoseesteren : 15 DK 173556 B1 r13 rl C -Glucose ^3C-NMR-Spektrum: (ppm) = 97,13 (d, C-Ιβ); 93,32 (d, C-1a); 77,63 (t, C-5P); 76,92 (t, C-3&); 75,57 (t, C-28); 73,84 (t, C-3a); 72,92 (t, C-2o); 72,24 (t, C-5o); 71,07 (t, C-4a); 70,63 (t, C-4P); 61,95 5 (dxd, 0-6αβ).The 13 NMR signal for the C-glucose starting material was compared with the 13 signal for the C-glucose ester: C-Glucose-3 93.32 (d, C-1a); 77.63 (t, C-5P); 76.92 (t, C-3 &); 75.57 (t, C-28); 73.84 (t, C-3a); 72.92 (t, C-20); 72.24 (t, C-50); 71.07 (t, C-4a); 70.63 (t, C-4P); 61.95 δ (dxd, 0-6αβ).

13 C -Glucoseesteren ifølge eksempel 2: 13C-NMR-Spektrum: (ppm) = 91,80 (m, C-Ίβ); 89,84 (m, C-1a); 72,51-66,73 (m, C-2,3,4,5a,β); 62,90 (m, C-6).13 C-The glucose ester of Example 2: 13 C-NMR Spectrum: (ppm) = 91.80 (m, C-Ίβ); 89.84 (m, C-1a); 72.51-66.73 (m, C-2,3,4,5a, β); 62.90 (m, C-6).

Da glucosesignalerne alle er brede multipletter, antages det, at gluco-10 sen var praktisk taget helt inkorporeret.Since the glucose signals are all broad multiples, it is believed that the glucose was practically fully incorporated.

Molforholdet lactid/glycolid/glucose = 32,3/66,7/0,2.The lactide / glycolide / glucose molar ratio = 32.3 / 66.7 / 0.2.

Ad eksempel 3: G PC-Bestemmelse med simultan UV- og radioaktivitetsbestemmelse blev anvendt til analyse af disse produkter. Det iagttages, at radioak-15 tiviteten i testprøven er proportionalt fordelt over hele molekylvægtsområdet, og at begge retentionstiderne i UV- og radioaktivitetsbestemmelserne er lige store.Example 3: G PC Determination with simultaneous UV and radioactivity determination was used for analysis of these products. It is observed that the radioactivity in the test sample is proportionally distributed over the entire molecular weight range and that both the retention times in the UV and radioactivity determinations are equal.

Radioaktiviteten i testprøven er ca. 30% af den forudsagte værdi, hvilket viser, at ca. 0,06% af glucosen blev inkorporeret (fra starten 20 var den 0,2%).The radioactivity in the test sample is approx. 30% of the predicted value, which shows that approx. 0.06% of the glucose was incorporated (from the beginning it was 0.2%).

EKSEMPEL 6EXAMPLE 6

Det ifølge eksempel 4 fremstillede produkt blev opløst i methylendi-chlorid og renset ved membranfiltrering under et tryk på 2 atmosfærer.The product of Example 4 was dissolved in methylene dichloride and purified by membrane filtration under a pressure of 2 atmospheres.

16 DK 173556 B116 DK 173556 B1

Amiconappa ratu r.Amiconappa ratu r.

Membran: DDS 6000 mwco.Diaphragm: DDS 6000 mwco.

Type FS 81 PP.Type FS 81 PP.

Strømningshastighed: 2,2 m!/minut.Flow rate: 2.2 m / min.

5 Slutvolumen: 2000 ml.Final volume: 2000 ml.

Remanens: Fra NMR:Residue: From NMR:

Mw = 42.200 Mw/Mn = 1,35 lactid/glycolid = 53/47 (molforhold)Mw = 42,200 Mw / Mn = 1.35 lactide / glycolide = 53/47 (molar ratio)

Mn = 31.300 10 Syretal: 3,4Mn = 31,300 Oxygen Number: 3.4

Ikke-omsat lactid <0,2%Unreacted lactide <0.2%

Ikke-omsat glycolid <0,4%Unreacted glycolide <0.4%

Filtrat: Fra NMR: 15 Mw = 21.600 Mw/Mn = 1,58 lactid/glycolid = 53/46 Cmolforhold)Filtrate: From NMR: 15 Mw = 21,600 Mw / Mn = 1.58 lactide / glycolide = 53/46 Cmol ratio)

Mn = 13.600Mn = 13,600

Syretai: 10,1Acid: 10.1

Ikke-omsat lactid <1,2%Unreacted lactide <1.2%

Ikke-omsat glycolid <0,4% 20__ EKSEMPEL 7 39,7 g (0,342 mol) diglycolid, 60,3 g (0,419 mol) diiactid, 0,2 g (1,1 millimol) D(*)-glucose (0,2%) og 40 m! toluen opvarmes til kogetemperatur (108°C) i en 750 ml's kolbe under omrøring, hvorefter der 17 DK 173556 B1 tilsættes 0,5 ml Sn-octoat. Reaktionen er let exoterm. Temperaturen stiger til 112°C. Efter 3 timer afbrydes omrøringen, og den brune viskose blanding videreomsættes i 3 dage ved 110°C. Efter afkøling tilsættes 500 ml methylendichlorid, og blandingen fortyndes ved koge-5 temperatur, renses med HYFLO® og filtreres.Unreacted Glycolide <0.4% EXAMPLE 7 39.7 g (0.342 mole) of diglycolide, 60.3 g (0.419 mole) of diactide, 0.2 g (1.1 millimole) of D (*) - glucose (0 , 2%) and 40 m! toluene is heated to boiling temperature (108 ° C) in a 750 ml flask with stirring, then 0.5 ml Sn-octoate is added. The reaction is slightly exothermic. The temperature rises to 112 ° C. After 3 hours, stirring is stopped and the brown viscous mixture is continued for 3 days at 110 ° C. After cooling, 500 ml of methylene dichloride is added and the mixture is diluted at boiling temperature, purified with HYFLO® and filtered.

Opløsningen inddampes til tørhed, og remanensen opløses i methylendichlorid og rystes med 400 ml 5%’s vandig HCI-opløsning. Opløsningen vaskes fire gange med 400 ml vand til pH-vaerdi 5 og fortyndes til 1 liter med methylendichlorid.The solution is evaporated to dryness and the residue is dissolved in methylene dichloride and shaken with 400 ml of 5% aqueous HCl solution. The solution is washed four times with 400 ml of water to pH 5 and diluted to 1 liter with methylene dichloride.

10 Opløsningen tørres med MgSO^ og inddampes til tørhed i vakuum ved 40°C. Remanensen tørres i vakuur ved 40°C.The solution is dried with MgSO4 and evaporated to dryness in vacuo at 40 ° C. The residue is dried in vacuo at 40 ° C.

Molekylvægt: Mw = 32.200; Mn = 18.400; Mw/Mn = 1,75.Molecular weight: Mw = 32,200; Mn = 18,400; Mw / Mn = 1.75.

NMR- og IR-spektrum: Som i eksempel 1.NMR and IR spectrum: As in Example 1.

EKSEMPEL 8 15 Analogt med det i eksempel 7 beskrevne fremstilles nedenstående polyolester i 345 ml toluen.EXAMPLE 8 Analogously to that described in Example 7, the following polyol ester is prepared in 345 ml of toluene.

Polyol: 0,6 g D(+)-glucose (0,2%) DL-Dilactid: 180,9 gPolyol: 0.6 g D (+) - glucose (0.2%) DL-Dilactide: 180.9 g

Diglycolid: 119,1 g 20 Sn-Octoat: 1,5 mlDiglycolide: 119.1 g Sn-Octoate: 1.5 ml

Reaktions-reaction

temp.: 114,1°Ctemp: 114.1 ° C

Mw: 20.000MW: 20,000

Mn: 12.000 25 Mw/Mn: 1,66Mn: 12,000 25 Mw / Mn: 1.66

Molforhold lactid/glycolid:Mole ratio of lactide / glycolide:

Syretal: 7,2Acid number: 7.2

Ikke-omsat: 30 lactid og <0,1% glycolid <0,4% 18 DK 173556 B1 EKSEMPEL 9Non-reacted: 30 lactide and <0.1% glycolide <0.4% 18 EXAMPLE 9

Analogt med det i eksempel 6 beskrevne fremstilles nedenstående produkt ved membranfiltrering ud fra det i eksempel 8 fremstillede produ kt: 5 Strømningshastighed: 1 ml/minut.Analogous to that described in Example 6, the following product is prepared by membrane filtration from the product of Example 8: Flow rate: 1 ml / minute.

Slutvoiumen: 2200 mlFinal volume: 2200 ml

Remanens: Fra NMR:Residue: From NMR:

Mw = 26.200 Mw/Mn = 1,45 lactid/glycolid = 62/37 (molforhold) 10 Mn = 18.000Mw = 26,200 Mw / Mn = 1.45 lactide / glycolide = 62/37 (molar ratio) 10 Mn = 18,000

Syretal: 4,0Acid number: 4.0

Ikke-omsat lactid <0,2%Unreacted lactide <0.2%

Ikke-omsat glycolid <0,4% 15 Filtrat: Fra NMR:Unreacted glycolide <0.4% Filtrate: From NMR:

Mw = 12.200 Mw/Mn = 3,75 lactid/glycolid = 60/40 (molforhold)Mw = 12,200 Mw / Mn = 3.75 lactide / glycolide = 60/40 (molar ratio)

Mn = 3.300Mn = 3,300

Syretal: 9,7Acid number: 9.7

Ikke-omsat lactid <0,2% 20 Ikke-omsat glycolid <0,4% 19 DK 173556 B1Unreacted lactide <0.2% 20 Unreacted glycolide <0.4% 19 DK 173556 B1

Polyolester ud fra β-cyclodextrine, DL-dilactid og diglycolid EKSEMPEL 10 26,1 g diglycolid, 39,6 g DL-dilactid og 0,635 g β-cyclodextrin opvarmes til 140°C i en kolbe under omrøring i nitrogenatomosfære, hvoref-5 ter der tilsættes 0,125 ml Sn-octoat. Reaktionen er udpræget exoterm. Temperaturen stiger til 180°C. Efter 10 minutter afbrydes omrøringen, og den brune viskose blanding videreomsættes ved 140°C i 17 timer.Polyolester from β-cyclodextrin, DL-dilactide and diglycolide EXAMPLE 10 26.1 g of diglycolide, 39.6 g of DL-dilactide and 0.635 g of β-cyclodextrin are heated to 140 ° C in a flask with stirring in a nitrogen atom, after which 0.125 ml of Sn-octoate is added. The reaction is markedly exothermic. The temperature rises to 180 ° C. After 10 minutes, stirring is stopped and the brown viscous mixture is continued at 140 ° C for 17 hours.

Rensningen og isoleringen udføres på analog måde som beskrevet i eksempel 1.The purification and isolation is performed in an analogous manner as described in Example 1.

10 Molekylvægt (GPC): Mw = 75.700; Mn = 72.300; Mw/Mn = 1,05.Molecular Weight (GPC): Mw = 75,700; Mn = 72,300; Mw / Mn = 1.05.

Ikke-omsat lactid: 2%. lkke-omsat glycolid: <0,4%.Unreacted lactide: 2%. Non-reacted glycolide: <0.4%.

Molforhold glycolid/lactid i polymer kæderne: 47/53.Mole ratio glycolide / lactide in the polymer chains: 47/53.

NMR- og IR-spektrum: Som i eksempel 1.NMR and IR spectrum: As in Example 1.

15 EKSEMPEL 11EXAMPLE 11

Analogt med det i eksempel 3 beskrevne fremstilles nedenstående polyolester:Analogous to that described in Example 3, the following polyol esters are prepared:

Polyol: 0,63 g β-cyclodextrin.Polyol: 0.63 g of β-cyclodextrin.

DL-Dilactid: 39,6 g.DL-Dilactide: 39.6 g.

20 Diglycolid: 26,1 g.Diglycolide: 26.1 g.

Sn-Octoat: 0,13 ml.Sn-Octoat: 0.13 ml.

Reaktionstemperatur: 165,8°C.Reaction temperature: 165.8 ° C.

Mw: 16.200; Mn: 5.100.Mw: 16,200; Mn: 5,100.

Mw/Mn: 3,18.Mw / Mn: 3.18.

25 Molforhold lactid/glycolid: 54/46.Mole ratio of lactide / glycolide: 54/46.

Syretal: 1,7.Acid number: 1.7.

Ikke-omsat lactid: <0,2%. lkke-omsat glycolid: <0,4%.Unreacted lactide: <0.2%. Non-reacted glycolide: <0.4%.

20 DK 173556 B1 EKSEMPEL 12EXAMPLE 12

Analogt med det i eksempel 3 beskrevne fremstilles nedenstående polyolester:Analogous to that described in Example 3, the following polyol esters are prepared:

Polyol: 0,63 g β-cyclodextrln tørret ved 120°C i vakuum.Polyol: 0.63 g of β-cyclodextrin dried at 120 ° C in vacuo.

5 DL-Dilactid: 39,6 g.DL-Dilactide: 39.6 g.

Diglycolid: 26,1 g.Diglycolide: 26.1 g.

Sn-Octoat: 0,13 ml.Sn-Octoat: 0.13 ml.

Reaktionstemperatur: 163,9°C.Reaction temperature: 163.9 ° C.

Mw: 24.100; Mn: 10.700.Mw: 24,100; Mn: 10,700.

10 Mw/Mn: 2,26.10 Mw / Mn: 2.26.

Molforhold lactid/glycolid: 53/47.Mole ratio of lactide / glycolide: 53/47.

Syretal: 6,2.Oxygen number: 6.2.

Ikke-omsat lactid: <0,2%.Unreacted lactide: <0.2%.

Ikke-omsat glycolid: <0,4%.Unreacted glycolide: <0.4%.

15 EKSEMPEL 13EXAMPLE 13

Det ifølge eksempel 10 fremstillede produkt behandles analogt med det i eksempel 6 beskrevne. Filtreringstrykket forøges imidlertid til 3 atmosfærer.The product of Example 10 is treated analogously to that of Example 6. However, the filtration pressure is increased to 3 atmospheres.

Strømningshastighed: 0,2 ml/minut.Flow rate: 0.2 ml / minute.

20 _____20 _____

Remanens: Fra nmR:Residue: From nmR:

Mw = 72.200 Mw/Mn = 1,20 lactid/glycolid = 53/47 (molforhold)Mw = 72,200 Mw / Mn = 1.20 lactide / glycolide = 53/47 (molar ratio)

Mn = 59.800Mn = 59,800

Syretal: 1,0 25__ 21 DK 173556 B1Acid Number: 1.0 25__ 21 DK 173556 B1

Filtrat: Fra NMR:Filtrate: From NMR:

Mw = 27.100 Mw/Mn = 1,75 lactid/glycolid = 52/48 (molforhold)Mw = 27,100 Mw / Mn = 1.75 lactide / glycolide = 52/48 (molar ratio)

Mn = 15.500Mn = 15,500

Syretal: 21,2 5 _ EKSEMPEL 14Oxygen Number: 21.2 EXAMPLE 14

Det ifølge eksempel 10 fremstillede produkt behandles analogt med det i eksempel 6 beskrevne. Filtreringstrykket forøges imidlertid til 2 atmosfærer.The product of Example 10 is treated analogously to that of Example 6. However, the filtration pressure is increased to 2 atmospheres.

10 Strømningshastighed: 0,3 ml/minut.Flow rate: 0.3 ml / minute.

Remanens:Residue:

Mw = 76.700 Mw/Mn = 1,06Mw = 76,700 Mw / Mn = 1.06

Mn = 72.300 15 ..._Mn = 72,300 15 ..._

Filtrat:filtrate:

Mw = 67.900 Mw/Mn = 1,43Mw = 67,900 Mw / Mn = 1.43

Mn = 47.600 20 EKSEMPEL 15Mn = 47,600 EXAMPLE 15

Lige store mængder af remanenserne fra eksempel 13 og 14 førte, efter mellemliggende opløsning i methylendichlorid, til en blanding med nedenstående sammensætning: 22 DK 173556 B1Equal amounts of the residues of Examples 13 and 14, after intermediate solution in methylene dichloride, resulted in a mixture of the following composition: 22 DK 173556 B1

Mw = 70.000 Mw/Mn = 1,36Mw = 70,000 Mw / Mn = 1.36

Mn = 51.600 EKSEMPEL 16-17Mn = 51,600 EXAMPLES 16-17

Polyolester ud fra D-(-)-mannitol, DL-dilactid og digiycolid 5 Analogt med den i eksempel 1 beskrevne fremgangsmåde blev nedenstående polyolestere fremstillet:Polyolester from D - (-) - mannitol, DL-dilactide and digiycolide 5 By analogy to the procedure described in Example 1, the following polyol esters were prepared:

Eks. 16 17* 10 Polyol 0,1 g D(-)-mannitol (0,2%) 5,0 g D(-)-mannitol (10%) DL-Dilactid 30,15 g 30,15 gEx. 16 17 * 10 Polyol 0.1 g D (-) - mannitol (0.2%) 5.0 g D (-) - mannitol (10%) DL-Dilactide 30.15 g 30.15 g

Digiycolid 19,85 g 19,85 g 15__Digiycolid 19.85 g 19.85 g 15__

Sn-Octoat 0,25 ml 0,25 mlSn-Octoat 0.25 ml 0.25 ml

Reak.temp. 177,5°C 176,5°CReak.temp. 177.5 ° C 176.5 ° C

20 Mw 23,500 3.50020 Mw 23,500 3,500

Mn 13.200 3.000Mn 13,200 3,000

Mw/Mn 1,78 1,13 25 _Mw / Mn 1.78 1.13 _

Molforhold lactid/glycolid 54:46 54:46Mole ratio of lactide / glycolide 54:46 54:46

Syretal 6,2 1,4 30 _ 23 DK 173556 B1Acid number 6.2 1.4 30 _ 23 DK 173556 B1

Eks. 16 17* I kke-omsat 5 lactid og <0,1% <0,2% glycolid <0,4% <0,4% * Til analyseformål,.jfr. nedenfor.Ex. 16 17 * In non-reacted 5 lactide and <0.1% <0.2% glycolide <0.4% <0.4% * For analytical purposes, cf. below.

EKSEMPEL 18-23 10 Polyolester ud fra polyoler, DL-dilactid og diglycolidEXAMPLES 18-23 10 Polyolester from polyols, DL-dilactide and diglycolide

Analogt med den i eksempel 1 beskrevne fremgangsmåde blev nedenstående polyolestere fremstillet:By the procedure described in Example 1, the following polyol esters were prepared:

Eks. 18 19* 20 21 22 23 15 -Ex. 18 19 * 20 21 22 23 15

Polyol 0,5 g 5 g 0,1 g 0,1 g 0,1 g 0,1 g penta- penta- sorbi- ribi- xyli- D(-)- erythritol erythritol tol tol tol fructose (1%) (10%) (0,2%) (0,2%) (0,2%) (0,2%) 20 _ DL-Di- 30,15 g 30,15 g 30,15 g 30,15 g 30,15 g 30,15 g lactidPolyol 0.5 g 5 g 0.1 g 0.1 g 0.1 g 0.1 g penta-penta-sorbibrixyxy-D (-) - erythritol erythritol tol tol tol fructose (1%) (10) %) (0.2%) (0.2%) (0.2%) (0.2%) 20-DL-Di-30.15 g 30.15 g 30.15 g 30.15 g 30, 15 g 30.15 g lactide

Digly- 19,85 g 19,85 g 19,85 g 19,85 g 19,85 g 19,85 g 25 colidDigly 19.85 g 19.85 g 19.85 g 19.85 g 19.85 g 19.85 g 25 colid

Sn-Oc- 0,25 ml 0,25 ml 0,25 ml 0,25 ml 0,25 mi 0,25 ml toatSn-Oc 0.25 ml 0.25 ml 0.25 ml 0.25 ml 0.25 ml 0.25 ml toat

30 Reak.- 132,5°C 154,5°C 179,1°C 159,7°C 156,6°C 175°CReact 132.5 ° C 154.5 ° C 179.1 ° C 159.7 ° C 156.6 ° C 175 ° C

temp.temp.

Mw 14.800 2.740 35.600 16.080 15.600 21.900 24 DK 173556 B1VAT 14,800 2,740 35,600 16,080 15,600 21,900 24 DK 173556 B1

Eks. 18 19* 20 21 22 23Ex. 18 19 * 20 21 22 23

Mn 10.000 2.450 20.500 6.800 6.000 12.700 5_____Mn 10,000 2,450 20,500 6,800 6,000 12,700 5_____

Mw/Mn 1,49 1,12 1,74 2,38 2,60 1,73Mw / Mn 1.49 1.12 1.74 2.38 2.60 1.73

Molforhold lactid/- 10 glycolid 54:46 57:43 54:46Mole ratio of lactide / - 10 glycolide 54:46 57:43 54:46

Syretal 7,5 0,73 I kke-omsat 15 lactid og 0,4% <0,1% <0,1% glycolid 0,1% <0,4% <0,4% * Til analyseformål, jfr. nedenfor.Acid number 7.5 0.73 In non-reacted 15 lactide and 0.4% <0.1% <0.1% glycolide 0.1% <0.4% <0.4% * For analysis purposes, cf. below.

Ad eksempel 17: 20 NMR-Spektrum (CDCI^) δ (ppm) = 5,23 (m, -CH- i mælkesyre, 1H); 4,83 (m, -Cf^- glycol-syre, 1,73H); 4,46-4,17 (m, -CH- og -CHi mannitol og i de terminale mælkesyre- eller glycolsyreenheder)Example 17: 20 NMR Spectrum (CDCl3) δ (ppm) = 5.23 (m, -CH- in lactic acid, 1H); 4.83 (m, -Cf- - glycolic acid, 1.73H); 4.46-4.17 (m, -CH- and -CHi mannitol and in the terminal lactic or glycolic acid units)

Molforhold: lactid/glycolid/mannitol = 1/0,86/0,08.Mole ratio: lactide / glycolide / mannitol = 1 / 0.86 / 0.08.

25 Dette svarer til en Mw på 1530 (signalet 4,46-4,17 omfatter imidlertid også de terminale mælkesyre- eller glycolsyreenheder).This corresponds to an Mw of 1530 (however, the signal 4.46-4.17 also includes the terminal lactic or glycolic acid units).

Anvendt mængde mannitol 672 x 10 ^ mol%; inkorporeret mængde 526 x 10 4 mol%.Amount of mannitol used 672 x 10 6 mol%; incorporated amount 526 x 10 4 mol%.

Ad eksempel 19: 25 DK 173556 B1 NMR-Spektrum (CDCIg) δ (ppm) = 5,23 (m, -CH- i mælkesyre, IH); 4,9-4,65 (m, -CH2* i glycolsyre, 1,5H); 4,45-4,10 (m, -CH2* i pentaerythritol og -CH- og -CHrf i de terminale mælkesyre- eller glycolsyreenheder, IH); 1,58 5 (m, CH2 i mælkesyre, 3H).For Example 19: 25 NMR Spectrum (CDCl 3) δ (ppm) = 5.23 (m, -CH- in lactic acid, 1H); 4.9-4.65 (m, -CH2 + in glycolic acid, 1.5H); 4.45-4.10 (m, -CH2 * in pentaerythritol and -CH- and -CHrf in the terminal lactic or glycolic acid units, 1H); 1.58 δ (m, CH 2 in lactic acid, 3H).

Molforhold: lactid/glycolid/pentaerythritol: 1/0,75/0,15 (signalet 4,45-4,10 omfatter imidlertid også de terminale mælkesyre- eller glycolsyreenheder) .Mole ratio: lactide / glycolide / pentaerythritol: 1 / 0.75 / 0.15 (however, the signal 4.45-4.10 also includes the terminal lactic acid or glycolic acid units).

Anvendt mængde pentaerythritol 960 x 10 ^ mol%, inkorporeret mæng-10 de (ifølge NMR) = 1000 x 10 ^ mol% (signalerne ved 4,45-4,10 er ikke udelukkende relateret til pentaerythritol).Quantity of pentaerythritol used is 960 x 10 6 mol%, incorporated amount (according to NMR) = 1000 x 10 6 mol% (the signals at 4.45-4.10 are not exclusively related to pentaerythritol).

Bestemmelse af nedbrydningen af polyolester In vitro EKSEMPEL 24 30-80 pm tykke film støbes af 5%’s opløsninger af polyofesteren ifølge 15 eksempel 6 i methylendichlorid. Filmene tørres i 50 timer ved 40°C i vakuum og derefter i flere dage i en exsiccator indeholdende P20^.Determination of the Degradation of Polyolester In vitro EXAMPLE 24 30-80 µm thick films are cast from 5% solutions of the polyofester of Example 6 in methylene dichloride. The films are dried for 50 hours at 40 ° C in vacuo and then for several days in a desiccator containing P 2 O 2.

300 mg af filmen delt i små stykker blev sat til 30 ml destilleret vand og rystet ved 37°C (50 rpm).300 mg of the film divided into small pieces was added to 30 ml of distilled water and shaken at 37 ° C (50 rpm).

Polymermængden blev bestemt periodisk ved filtrering og vejning.The amount of polymer was determined periodically by filtration and weighing.

20 EKSEMPEL 25EXAMPLE 25

Implantater i form af tabletter med en diameter på 7 mm og med en vægt på 23-25 mg, presset af et polyolestergranulat ifølge eksempel 6 ved 80 bar og 75°C i 10 minutter blev implanteret intraperitonealt i rotter. Efter en bestemt tid blev de ekstraheret fra vævet med meth-25 ylendichlorid og derved skilt fra det organiske vævsmateriale, inddampet til tørhed og vejet.Implants in the form of tablets having a diameter of 7 mm and weighing 23-25 mg, pressed by a polyol ester granulate of Example 6 at 80 bar and 75 ° C for 10 minutes, were implanted intraperitoneally in rats. After a certain time, they were extracted from the tissue with methylene dichloride and thereby separated from the organic tissue material, evaporated to dryness and weighed.

26 DK 173556 B126 DK 173556 B1

Frigørelse af aktive midler fra polyolestermatrixer in vitro EKSEMPEL 26Release of active agents from polyol ester matrices in vitro Example 26

Frigørelsestests blev udført med mikrokapsler, som indeholdt bromo-cryptin som aktivt middel. Mikrokapslerne blev fremstillet ved den 5 ovenfor beskrevne spraytørringsmetode med følgende parametre:Release tests were performed with microcapsules containing bromo-cryptin as active agent. The microcapsules were prepared by the spray drying method described above with the following parameters:

Bromocryptin-mesyfat 2,6 gBromocryptin mesyfat 2.6 g

Matrixpolymer ifølge eksempel 9 (remanens) 10,0 gMatrix polymer of Example 9 (residue) 10.0 g

Methylendichlorid 100 mlMethylene dichloride 100 ml

Spraybetingelser (NI RO-udstyr):Spray conditions (NI RO equipment):

10 Indgangstemperatur 50°CInlet temperature 50 ° C

Udgangstemperatur 40°CInitial temperature 40 ° C

Lufttryk 2 atmosfærerAir pressure 2 atmospheres

Strømningshastighed 32 ml/minut.Flow rate 32 ml / minute.

Efter fremstillingen blev mikrokapslerne tørret i 48 timer ved 30°C i 15 lavt vakuum, sigtet (<180 ym) og vasket med citratpuffer med pH-værdi 3. Mikrokapslerne indeholdt 17,9% af det aktive middel.After preparation, the microcapsules were dried for 48 hours at 30 ° C in low vacuum, sieved (<180 µm) and washed with citrate buffer of pH 3. The microcapsules contained 17.9% of the active agent.

Efter gentagen tørring i lavt vakuum (48 timer, 35°C, 0,1 bar) og sigtning (<180 ym) blev mikrokapslerne gammasteriliseret ved 2,5 Mrad.After repeated drying in low vacuum (48 hours, 35 ° C, 0.1 bar) and sieving (<180 µm), the microcapsules were gamma sterilized at 2.5 Mrad.

20 Frigørelsen blev målt fotometrisk ved 301 nm ved 25°C med citratpuffer, pH-værdi 4, som ekstraktionsmedium, og hældt frisk igennem mikrokapslerne med en strømningshastighed på 2,5 ml/minut.The release was measured photometrically at 301 nm at 25 ° C with citrate buffer, pH 4, as extraction medium, and poured freshly through the microcapsules at a flow rate of 2.5 ml / minute.

I løbet af 24 timer frigjordes ca. 62% af det aktive middel regelmæssigt.Within 24 hours, approx. 62% of the active agent regularly.

25 NB Frigørelsen in vitro blev målt ved pH 4 på grund af bromocryp-tins bedre opløselighed ved denne pH-værdi.25 NB The in vitro release was measured at pH 4 due to the better solubility of bromocryptine at this pH.

EKSEMPEL 27 27 DK 173556 B1EXAMPLE 27 27 DK 173556 B1

Frigørelsestests blev udført med mikrokapsler, som indeholdt coder-gocrin som aktivt middel.Release tests were performed with microcapsules containing coder-gocrin as active agent.

Mikrokapslerne blev fremstillet ved den ovenfor beskrevne emulsions-5 proces med nedenstående parametre:The microcapsules were prepared by the above-described emulsion process with the following parameters:

Codergocrinbase 7 gCodergocrin Base 7 g

Matrixpolymer ifølge eksempel 5 13 gMatrix polymer of Example 5 13 g

Methylendichlorid 40 mlMethylene dichloride 40 ml

Ethanol 94% 30 ml 10 Emulgeringsbetingelser:Ethanol 94% 30 ml Emulsification conditions:

Volumenforhold mellem organisk fase og vandig fase: 1:65 Rotationshastighed i omrøreren: p = 3100 rpm.Volume ratio of organic phase to aqueous phase: 1:65 Speed of rotation of the stirrer: p = 3100 rpm.

Frigørelsen blev målt som beskrevet i eksempel 26.The release was measured as described in Example 26.

EKSEMPEL 28 15 Den i eksempel 27 beskrevne fremgangsmåde blev udført med følgende parametre:EXAMPLE 28 The procedure described in Example 27 was carried out with the following parameters:

Ketotifenbase 5 gKetotifen Base 5 g

Matrixpolymer ifølge eksempel 5 15 gMatrix polymer of Example 5 15 g

Methylendichlorid 80 ml 20 Emulgeringsbetingelser:Methylene dichloride 80 ml Emulsification conditions:

Volumenforhold mellem organisk fase og vandig fase: 3:130 p = 2000 rpm.Volume ratio between organic phase and aqueous phase: 3: 130 p = 2000 rpm.

Omrøringstid: 2 timerStirring time: 2 hours

Mikrokapslerne indeholdt 16,5% ketotifen.The microcapsules contained 16.5% ketotifen.

28 DK 173556 B1 EKSEMPEL 29EXAMPLE 29

Frigørelse af aktive midler fra polyolestermatrixer in vivoRelease of active agents from polyol ester matrices in vivo

Der blev udført frigørelsestests med mikrokapsler, der som aktivt middel indeholdt bromocryptin.Microcapsule release capsules containing bromocryptin as active agent were performed.

5 Mikrokapslerne blev fremstillet ved den ovenfor beskrevne spraytørringsproces i et NI RO-spraytørringsapparatur forsynet med centrifugal spraydyse. Matrixpolymeren bestod af produktet ifølge eksempel 4 og indeholdt 17,8¾ bromocryptin.The microcapsules were prepared by the above-described spray drying process in a NI RO spray drying apparatus provided with centrifugal spray nozzle. The matrix polymer consisted of the product of Example 4 and contained 17.8¾ bromocryptin.

En portion af disse mikrokapsler, svarende til 5,0 mg bromocryptin-10 mesylat, i et bærestof af 0,2 ml natriumcarboxymethylcellulose blev injiceret i højre lårmuskel på en kanin. Der blev periodisk udtaget blodprøver fra kaninen i 21 dage.A portion of these microcapsules, corresponding to 5.0 mg of bromocryptine mesylate, in a carrier of 0.2 ml of sodium carboxymethyl cellulose was injected into the right thigh muscle of a rabbit. Blood samples were taken periodically from the rabbit for 21 days.

Blodniveauet for medikamentet blev målt ved en specifik radioimmunoassay og havde en middelvaerdi på 1,6 ng/ml (A.U.C. = 33,0). Blod-15 niveauerne lå praktisk taget alle mellem 1,20 og 1,80 ng/ml.The blood level of the drug was measured by a specific radioimmunoassay and had a mean value of 1.6 ng / ml (A.U.C. = 33.0). The blood-15 levels were practically all between 1.20 and 1.80 ng / ml.

Claims (9)

1. Ester af en polyol, hvilken polyol indeholder mindst tre hydroxygrupper og har en molekylvægt på op til 20.000, hvorhos mindst én hydroxygruppe i denne polyol er i · 5 form af en ester, med en poly- eller co-polymælkesyrerest, som hver har en molekylvægt på mindst 5000.An ester of a polyol, said polyol containing at least three hydroxy groups and having a molecular weight of up to 20,000, wherein at least one hydroxy group of said polyol is in the form of an ester, with a poly or co-poly lactic acid residue each having a molecular weight of at least 5000. 2. Reaktionsprodukt mellem en polyol indeholdende mindst 3 hydroxygrupper og med en molekylvægt på op til 20.000 eller et reaktivt derivat deraf og mælkesyre eller et 10 reaktivt derivat deraf og, om ønsket, mindst én yderligere hydroxycarboxylsyre eller et funktionelt derivat deraf, hvilket produkt har en polymerkæde med en molekylvægt på mindst 5000.A reaction product between a polyol containing at least 3 hydroxy groups and having a molecular weight of up to 20,000 or a reactive derivative thereof and lactic acid or a reactive derivative thereof and, if desired, at least one additional hydroxycarboxylic acid or functional derivative thereof, which product has a polymer chain having a molecular weight of at least 5000. 3. Produkt ifølge krav 1, kendetegnet ved, at polyolen er en polyol med 15 glucosestruktur.Product according to claim 1, characterized in that the polyol is a polyol having a glucose structure. 4. Produkt ifølge krav 1, kendetegnet ved, at det indeholder syrerester, som omfatter 30-70 molprocent glycolsyreenheder.Product according to claim 1, characterized in that it contains acid residues comprising 30-70 mole percent glycolic acid units. 5. Produkt ifølge krav 1, kendetegnet ved, at en hvilken som helst separat lavmolekylvægttop ifølge GPC udgør i alt op til 10% af højden af polyesterens MW-top.Product according to claim 1, characterized in that any separate low molecular weight peak according to GPC constitutes a total of up to 10% of the height of the polyester MW peak. 6. Fremgangsmåde til fremstilling af et produkt ifølge krav 1,kendetegnet ved, at en polyol med en molekylvægt på op til 20.000 og med mindst 3 hydroxygrupper eller 25 et reaktivt derivat deraf esterificeres med mælkesyre eller et reaktivt derivat deraf og, om ønsket, med mindst én yderligere hydroxycarboxylsyre eller et funk- tionelt derivat deraf.Process for the preparation of a product according to claim 1, characterized in that a polyol having a molecular weight of up to 20,000 and having at least 3 hydroxy groups or a reactive derivative thereof is esterified with lactic acid or a reactive derivative thereof and, if desired, with at least one additional hydroxycarboxylic acid or a functional derivative thereof. 7. Depotmatrixmateriale af et produkt ifølge krav 1, kendetegnet ved, at det 30 indeholder en farmakologisk aktiv forbindelse. 1 Depotmatrixmateriale af et produkt ifølge krav 7, kendetegnet ved, at de indeholder bromocryptin, ketotifen eller codergocrin som farmaceutisk aktivt middel. DK 173556 B1Depot matrix material of a product according to claim 1, characterized in that it contains a pharmacologically active compound. Depot matrix material of a product according to claim 7, characterized in that they contain bromocryptin, ketotifen or codergocrine as a pharmaceutically active agent. DK 173556 B1 9. Parenteralt farmaceutisk depotpræparat til anvendelse som implantat eller mikrokapsler indeholdende et farmakologisk aktivt middel indlejret i eller indkapslet i en polymermatrix af en ester af en polyol ifølge krav 1, hvilket præparat er tildannet til at frigøre alt eller i det væsentlige alt aktivt stof i et forlænget tidsrum, og polymeren er 5 tildannet således, at den nedbrydes tilstrækkeligt hurtigt til at blive transporteret væk fra administrationsstedet inden for 20 dage efter frigørelse af alt eller i det væsentlige alt det aktive middel.A parenteral pharmaceutical depot composition for use as an implant or microcapsules containing a pharmacologically active agent embedded in or encapsulated in a polymer matrix of an ester of a polyol according to claim 1, which composition is formed to release all or substantially all of the active substance into a drug. prolonged period of time and the polymer is formed such that it degrades sufficiently rapidly to be transported away from the site of administration within 20 days of release of all or substantially all of the active agent. 10. Præparat ifølge krav 9, kendetegnet ved, at det indeholder bromocryptin, 10 ketotifen eller codergocrin som farmaceutisk aktivt middel.Composition according to claim 9, characterized in that it contains bromocryptine, ketotifen or codergocrine as a pharmaceutically active agent.
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FR2551072A1 (en) 1985-03-01
IL72763A0 (en) 1984-11-30
AU575066B2 (en) 1988-07-21
SE462098B (en) 1990-05-07
ES535399A0 (en) 1987-06-16
JPH0819226B2 (en) 1996-02-28
GB2145422B (en) 1987-08-26
US5922682A (en) 1999-07-13
BE900406A (en) 1985-02-22
NL8402547A (en) 1985-03-18
IE842171L (en) 1985-02-26
SG53590G (en) 1990-10-26
CH656884A5 (en) 1986-07-31
ES8706750A1 (en) 1987-06-16
PH23556A (en) 1989-08-25
GB2145422A (en) 1985-03-27
PT79129A (en) 1984-09-01
NL960014I1 (en) 1996-10-01
GB8421273D0 (en) 1984-09-26
ZA846634B (en) 1986-04-30
GR80184B (en) 1985-01-02
IT1176629B (en) 1987-08-18
AU3234884A (en) 1985-02-28
JPS6076531A (en) 1985-05-01
HU195426B (en) 1988-05-30
SE8404225L (en) 1985-02-27
IL72763A (en) 1988-02-29
NL190415B (en) 1993-09-16
AT395584B (en) 1993-01-25
MY101861A (en) 1992-01-31
IE58818B1 (en) 1993-11-17
DK407284A (en) 1985-02-27
CY1556A (en) 1991-03-22
SE8404225D0 (en) 1984-08-24
DE3430852C2 (en) 2003-08-14
LU85514A1 (en) 1985-04-24
ATA271384A (en) 1992-06-15
US5922338A (en) 1999-07-13
IT8422413A0 (en) 1984-08-24
DE3430852A1 (en) 1985-03-14
PT79129B (en) 1986-07-17
NL190415C (en) 1994-02-16
HUT38265A (en) 1986-05-28
DK407284D0 (en) 1984-08-24
FR2551072B1 (en) 1988-01-15
HK67390A (en) 1990-09-07
NZ209335A (en) 1988-08-30

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